(498f) Optimization of LNT/SCR Aftertreatment Catalysts: Investigation of NH3 Storage/Release Dynamics Over Fe-Loaded Zeolites | AIChE

(498f) Optimization of LNT/SCR Aftertreatment Catalysts: Investigation of NH3 Storage/Release Dynamics Over Fe-Loaded Zeolites

Authors 

Feng, H. - Presenter, University of Michigan
Schwank, J. - Presenter, University of Michigan

Lean burn engines like spark ignition direct injection engines (SIDI)
offer significant fuel economy benefits and reduced CO2 emissions. A
major challenge is the difficulty of reducing effectively lean NOx
as the conventional three-way catalyst does not work for NOx
reduction under lean conditions. An aftertreatment system containing lean NOx
trap (LNT) catalysts provides one of the promising options to eliminate NOx
when the engine works under so-called lean–rich repeatable operation
cycles. LNT catalyst components store NOx during the lean cycle, and
then the stored NOx is released and catalytically reduced when the
engine operates under rich condition. Therefore, the role of LNT catalyst in
the both rich and lean cycles is equally critical in terms of the ultimate NOx
removal efficiency of aftertreatment systems.

During fuel
combustion in the engine, steam is generated and represents one of the major
components in automotive exhaust. While steam effects have been widely
investigated for TWC catalysts, less is known about how steam effects NOx
reduction over LNT catalysts. In previous studies, we found that during the
rich cycle the primary NOx reduction product over Pt–BaO/Al2O3
was NH3. Based on results from combined temperature programmed
reduction of stored NOx by H2 and from measurements of
the NOx reduction efficiency and NH3 selectivity versus
reaction temperature over Pt–BaO/Al2O3, we
suggested that steam causes NH3 formation via the reduction of NOx
by H2 that is generated by water gas shift when CO used as reductant
or by steam reforming when hydrocarbon (C3H8) used as
reductant. Thus, a method was established using a dual-bed reactor system
containing a zeolite catalyst down-stream of the LNT bed to capture NH3
generated during the rich cycle. The zeolite serves then as NH3-SCR catalyst
to eliminate lean NOx by using desorbed NH3 as reductant
when the rich cycle is switched to the lean cycle.

Zeolites,
particularly Fe- and Cu-containing ZSM-5 and Beta, have showed remarkable lean
NOx reduction ability for NH3 used as reductant (NH3-SCR).
So far, extensive NH3-SCR studies have been carried out over these
types of zeolite catalysts. However, many fundamental issues are still poorly
understood regarding the use of NH3 generated during the LNT rich
cycle to further reduce NOx in the lean cycle over zeolite
catalysts. In order to optimize LNT/SCR aftertreatment systems for SIDI
application, in this work, NH3 storage/release will be investigated
over zeolites and compared with Fe-loaded zeolites that prepared using
different Fe loadings. The effects of preparation method, aging and operation
conditions on NH3 storage/release dynamics will also be evaluated.
The role and status of Fe species in zeolite will be discussed in light of the
performance of NH3 release or conversion.